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classificationCPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C9-16
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C5-2791
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C5-27
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C9-16
filingDate 1993-07-06-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 1994-11-15-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9dd288a91f083d176307186aa1a66714
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_109717673eb7d42ab229e3f5889d159d
publicationDate 1994-11-15-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber US-5364997-A
titleOfInvention Process for converting multi-branched heavy hydrocarbons to high octane gasoline
abstract The present invention relates to a process for upgrading multi-branched C 9 + olefinic and/or paraffinic by-products of heavy hydrocarbon upgrading processes including alkylation, polymerization, and MOGD, to high octane gasoline. Feeds rich in multi-branched C 9 + olefins and/or paraffins are contacted with hydrogen at a pressure in the range of about 200 psig to about 2000 psig in the presence of an unsulfided catalyst composition comprising a low acidity molecular sieve having an Alpha Value of 5 or less. Because of the capability of the catalyst to crack at unsubstituted carbon-carbon bonds, the paraffinic products are more highly branched, and thus higher in octane number than those obtained from conventional dual function hydrocracking catalysts having Alpha Values greater than 5.
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